Aiming at investigating fluid flowing behaviours in large scale multi-size bubbly flow
two population balance models
named Bubble Number Density Transfer(BNDT)model and Multi-Size-Group(MUSIG)model coupled with bubble coalescence and breakage mechanism respectively
are employed to simulate the MTLOOP(Multi-phase Loop)experiment with characteristics of coalescence dominating trends. In comparison to experimental data
both models are able to well capture the dynamic evolution trends of bubble diameter and transition of gas volume fraction distribution
but the computing period of BNDT gets shorter by 1/10~1/20 than that of MUSIG under the similar predictions
thus BNDT model is more appropriate for predicting large scale multi-size bubbly flow in rocket engineering.
关键词
Keywords
references
GNOTKE O, BENK H, LOTH R. Experimental study on the number density distribution function in turbulent bubbly flows with coalescence and break-up [J].Experimental Thermal and Fluid Science, 2003, 27(7): 803-816.
KUMAR S, RAMKRISHNA D. On the solution of population balance equation by discretization: I A fixed pivot technique [J]. Chem Eng Sci, 1996, 51(8): 1311-1332.
KOCAMUSTAFAOGULLSRI G, ISHII M. Foundation of the interfacial area transport equation and its closure relations [J].International Journal of Heat and Mass Transfer, 1995, 38(3): 481-493.
SOKOLICHIN A, EIGENBERGER G, LAPIN A, et al. Dynamic numerical simulation of gas-liquid two-phase flows Eular/Eular versus Eular/Lagrange [J]. Chem Eng Sci, 1997, 52(4): 611-622.
LUCAS D, KREPPER E, PRASSER H M. Prediction of radial gas profiles in vertical pipe flow on basis of the bubble size distribution [J]. International Journal of Thermal Sciences, 2001, 40(3): 217-225.
KREPPER E, LUCAS D, PRASSER H M. On the modeling of bubbly flow in vertical pipes [J].Nuclear Engineering and Design, 2005, 235(5): 597-611.
KREPPER E, LUCAS D, FRANK T, et al. The inhomogeneous MUSIG model for the simulation of polydispersed flows[J].Nuclear Engineering and Design, 2008, 238(7): 1690-1702.
WANG Tiefeng, WANG Jinfu, YANG Weiguo, et al. Experimental study on bubble size distribution in three-phase circulating fluidized beds[J]. Chemical Industry Engineering, 2001,52(3): 197-203.
WANG Xiaodong, ZHANG Zibo, TU Jiyuan. Numerical study on a simplified population balance approach for isothermal bubbly flow [J]. Acta Mechanica Sinica,2008,40(4):441-446.
CHEUNG S C P, YEOH G H, TU J Y. Population balance modeling of bubbly flows considering the hydrodynamics and thermomechanical processes [J]. American Institute of Chemical Engineers Journal, 2008, 54(7):1689-1710.
CHEUNG S C P, YEOH G H, TU J Y. On the numerical study of isothermal vertical bubbly flow using two population balance approaches[J].Chemical Engineering Science, 2007, 62(17): 4659-4674.
PRINCE M J, BLANCH H W. Bubble coalescence and break-up in air-sparged bubble columns[J]. American Institute of Chemical Engineers Journal, 1990, 36(10): 1485-1499.
LUO H, SVENDSEN H F. Theoretical model for drop and bubble break-up in turbulent flows[J]. American Institute of Chemical Engineers Journal, 1996, 42(5),: 1225-1233.
WU Q, KIM S, ISHII M, et al. One-group interfacial area transport in vertical bubbly flow[J]. Int J Heat Mass Trans, 1998, 41(8/9): 1103-1112.
LUCAS D, KREPPER E, PRASSER H M. Use of models for lift, wall and turbulent dispersion forces acting on bubbles for poly-disperse flows[J]. Chemical Engineering Science, 2007, 62(15): 4146-4157.
DREW D A, LAHEY J R T. Application of general constitutive principles to the derivation of multidimensional two-phase flow equation[J]. Int J Multiphase Flow, 1979, 5(4): 243-264.
ANSYS-CFX Development Team. Solver theory, multiphase flow theory [M]. Pittsburgh, PA, USA: ANSYS Inc., 2007.
MENTER F R. Two-equation eddy viscosity turbulence models for engineering applications[J]. AIAA Journal, 1994, 32(8): 1598-1605.
SATO Y, SADATOMI M, SEKOGUCHI K. Momentum and heat transfer in two-phase bubbly flow: I[J]. International Journal of Multiphase Flow, 1981, 7(2): 167-177.
LUCAS D, KREPPER E, PRASSER H M. Development of co-current air-water flow in a vertical pipe[J]. International Journal of Multiphase Flow, 2005, 31(12): 1304-1328.
SUN X D, KIMA S J, ISHII M, et al. Model evaluation of two-group interfacial area transport equation for confined upward flow[J]. Nuclear Engineering and Design, 2004, 230(1/3): 27-47.
Study of the Mechanism of Electrostatic Accumulation and Current Density Distribution Characteristics During Liquid Hydrogen Pipeline Transportation
Numerical Simulation of Space Charge Distribution Characteristics of Polyimide Materials under X-Ray Irradiation
Numerical Simulation Study on Geothermal Extraction Characteristics of Supercritical CO2 in Heterogeneous Fractures
Action Mechanism of Heat Transfer between the Working Medium and the Impeller on Aerodynamic Performance and Flow Characteristics of Radial Inflow Turbines with Supercritical Carbon Dioxide
Analysis of the Attached Vortex Model for the Flow Characteristics of Wing Near-Field Wakes
Related Author
SUN Wenhao
LIU Hongbao
WANG Lei
QING Ziyou
LI Zhuolun
MA Yuan
LI Yanzhong
ZHONG Hui
Related Institution
School of Energy and Power Engineering,Xi’an Jiaotong University
Aerospace System Engineering Shanghai
School of Electrical Engineering,Xi’an Jiaotong University
Northwest Institute of Nuclear Technology
Institute of Electronic Engineering,China Academy of Engineering Physics